Highly heat-resistant and highly transparent polycarbonate ester, and preparation method therefor

ABSTRACT

The present invention relates to: a bio-based polycarbonate ester comprising: (i) repeat unit 1 obtained from a condensation reaction of 1,4:3,6-dianhydrohexitol and carbonate; and (ii) repeat unit 2 obtained from a condensation reaction of 1,4:3,6-dianhydrohexitol and 1,4-cyclohexanedicarboxylate; and a preparation method for the bio-based polycarbonate ester, comprising the steps of: (1) preparing a compound represented by formula 3 through a trans-esterification or esterification reaction of a compound represented by formula 2 and phenol; and (2) preparing a compound comprising a repeat unit represented by formula 1 through a polycarbonate melt polycondensation reaction of the compound represented by formula 3 prepared in step (1), a compound represented by formula 4, and 1,4:3,6-dianhydrohexitol. The bio-based polycarbonate ester, according to the present invention, is capable of controlling advantages and disadvantages of physical properties obtained from each repeat unit, and has high thermal resistance and high transparency, and thus is capable of being effectively used for various uses.

FIELD OF THE INVENTION

The present invention relates to a polycarbonate ester having high heatresistance and transparency, and a preparation method thereof. Morespecifically, it relates to a biomass-based polycarbonate ester havingrepeating units which are obtained from a reaction of1,4:3,6-dianhydrohexitol and a carbonate or an1,4-cyclohexanedicarboxylate.

BACKGROUND OF THE INVENTION

Unlike conventional resources based on petrochemical industry,1,4:3,6-dianhydrohexitol is a bio-based material derived from a biomass,i.e., a renewable resource containing polysaccharide as its componentssuch as corn, wheat, sugar, and the like. Particularly, in case of abioplastic containing a bio-based material, carbon dioxide (CO₂)produced during waste disposal processes after the use of a bioplasticcan be reused for the growth of biomass, and thus the bioplastic hasbeen noticed as a carbon dioxide reduction material to prevent globalwarming, which is a serious worldwide issue.

1,4:3,6-Dianhydrohexitol exists in three different forms ofstereoisomers, which has different chemical properties depending on thedifference in the relative configuration of two hydroxyl groups presenttherein: isomannide (as shown in formula a below, mp: 81-85° C.),isosorbide (as shown in formula b below, mp: 61-62° C.), and isoidide(as shown in formula c below, mp: 64° C.). Particularly, in a case where1,4:3,6-dianhydrohexitol is used as a monomer material of polycarbonatewhich is one of representative engineering plastics, the polycarbonatethus prepared can have good thermal and optical properties owing tomolecular structural characteristics of 1,4:3,6-dianhydrohexitol, i.e.,rigidity and saturated heterocyclic structure, together with theadvantages of a bioplastic.

Since 1,4-dimethyl-cyclohexane dicarboxylate (hereinafter referred to asDMCD) or 1,4-cyclohexanedicarboxylic acid (hereinafter referred to asCHDA), a hydrolysis product of DMCD, has a cyclohexane ring structure inthe center of the molecule. Thus, if these materials are introduced intoa polymer chain, they improve the weatherability and UV stability of thepolymer, and also allow the polymer to have excellent materialproperties, such as gloss retention, yellowing resistance, hydrolyticstability, corrosion resistance, and chemical resistance, owing to itsunique combination of flexibility and hardness in the molecularstructure.

Poly(1,4-cyclohexylidene 1,4-cyclohexanedicarboxylate) (hereinafterreferred to as PCCD), a DMCD/CHDM homopolyester, is an example ofcommercially available polymer materials developed by using DMCD. Owingto its superior properties such as weatherability, chemical resistance,flowability, and a low refractive index, PCCD has been used to develop apolycarbonate/PCCD alloy (product name: Xyrex) by DuPont (USA) in orderto improve transparency of polycarbonate.

A commercial manufacturing process of polycarbonate can be divided intotwo processes: solution polymerization and melt polycondensation. Unlikethe solution polymerization process where phosgene is used as a sourcematerial for carbonate, diphenyl carbonate (hereinafter referred to asDPC) is used in the melt polycondensation process. Thus, raw materialsused in the conventional melt polycondensation process generally includeDPC and bisphenol A (hereinafter referred to as BPA), which is a diol;and a transesterification reaction of BPA with DPC produces phenol as abyproduct of the melt polycondensation.

Meanwhile, it is required to convert a functional group present in DMCDor CHDA into another functional group, which may cause the production ofphenol as a byproduct via a transesterification reaction with diol, inorder to use DMCD or CHDA in the polycarbonate melt polycondensation.For example, dimethyl ester of DMCD or dicarboxylic acid of CHDA needsto be converted into diphenyl ester. Thus, an example of diphenyl esterderivatives of DMCD or CHDA which can be used for the polycarbonate meltpolycondensation is 1,4-diphenyl-cyclohexanedicarboxylate (hereinafterreferred to as DPCD), and is synthesized by a reaction of DMCD or CHDAwith phenol, as represented by Reaction Scheme 1 below:

In general, in case of 1,4-dimethyl-terephthalate (a tertiary dimethylester) and terephthalic acid (a diacid), a reaction does not occurtherebetween if either one of their functional groups, i.e., one of acidand alcohol, is not activated. In case of DMCD (a secondary dimethylester) and CHDA (a diacid), however, they can react with phenol in amolten state, and thus it is easier to conduct DPCD synthesis.

The present invention employs DPCD, which is used as a material forforming an ester bond in the polymer chain, to provide anisosorbide-based polycarbonate ester (or polyester carbonate). Thepolycarbonate ester thus obtained is a novel bioplastic having high heatresistance and transparency whose properties and forming processabilitycan be adjusted according to its needs by varying the DPCD content. Thebio-based polycarbonate ester according to the present invention canexhibit the same level of heat resistance as compared to theconventional bioplastic disclosed in US 2011/0003101 A1, even comprisinga less amount of isosorbide, and thus have a relative advantage in termsof production costs.

SUMMARY OF THE INVENTION

Therefore, it is an object of the present invention to provide abio-based polycarbonate ester having high heat resistance andtransparency with a high degree of polymerization and good mechanicalproperties, comprising a rigid polymer repeating unit with no BPAcausing an environmental hormone, which is useful in variousapplications, e.g., glass alternative for automobile, optical lens andfilm, feeding bottle, food container, etc. In addition, it is anotherobject of the present invention to provide a preparation method of thebio-based polycarbonate ester.

In accordance with one aspect of the present invention, there isprovided a bio-based polycarbonate ester comprising: (i) Repeating Unit1 obtained from a condensation reaction of 1,4:3,6-dianhydrohexitol anda carbonate; and (ii) Repeating Unit 2 obtained from a condensationreaction of 1,4:3,6-dianhydrohexitol and an1,4-cyclohexanedicarboxylate.

In accordance with another aspect of the present invention, there isprovided a method for manufacturing a bio-based polycarbonate estercomprising the steps of:

(1) subjecting a compound of formula 2 and phenol to atransesterification or esterification reaction to obtain a compound offormula 3; and (2) subjecting the compound of formula 3 obtained in Step(1), a compound of formula 4, and 1,4:3,6-dianhydrohexitol to apolycarbonate melt polycondensation reaction to prepare a compoundcomprising a repeating unit of formula 1:

wherein, in formula 1, x satisfies 0<x<1,

in formula 2, R is methyl or hydrogen, and,

in formula 4, R₁ and R₂ are each independently an aliphatic group having1 to 18 carbon atoms or an aromatic group having 6 to 20 carbon atomswhich may have an optional substituent.

The bio-based polycarbonate ester according to the present inventionexhibits high heat resistance and transparency, and has an advantagethat properties deriving from (i) Repeating Unit 1 obtained from acondensation reaction of 1,4:3,6-dianhydrohexitol and a carbonate, and(ii) Repeating Unit 2 obtained from a condensation reaction of1,4:3,6-dianhydrohexitol and an 1,4-cyclohexanedicarboxylate can becontrolled by regulating the contents thereof.

Thus, the inventive bio-based polycarbonate ester can be useful invarious applications such as glass alternative for automobile, opticallens and film, feeding bottle, food container, etc.

BRIEF DESCRIPTION OF THE DRAWINGS

The above and other objects, features and other advantages of thepresent invention will be more clearly understood from the followingdetailed description taken in conjunction with the accompanyingdrawings, in which:

FIG. 1 is a graph showing the change in glass transition temperature(Tg) of polymers depending on the content ratio of DPC.

FIG. 2 is an ¹H NMR spectrum of a bio-based polycarbonate ester preparedin Example 1.

FIG. 3 is an IR spectrum of a bio-based polycarbonate ester prepared inExample 1.

DETAILED DESCRIPTION OF THE INVENTION

Hereinafter, the present invention will be described in detail.

A bio-based polycarbonate according to the present invention comprises(i) Repeating Unit 1 obtained from a condensation reaction of1,4:3,6-dianhydrohexitol and a carbonate, and (ii) Repeating Unit 2obtained from a condensation reaction of 1,4:3,6-dianhydrohexitol and an1,4-cyclohexanedicarboxylate, and may comprises a repeating unit offormula 1 below:

wherein x satisfies 0<x<1.

In the repeating unit of formula 1 above, the ratio of cis/transcyclohexanedicarboxylate unit may be 1/99% to 99/1%, preferably 20/80%to 80/20%, more preferably 30/70% to 70/30%.

When the content of trans cyclohexanedicarboxylate unit increases, heatresistance improves owing to an increase in the glass transitiontemperature (Tg) although transparency relatively decreases. Incontrast, if there is a decrease in the content of transcyclohexanedicarboxylate unit, transparency improves while there is areduction in heat resistance due to a decrease in Tg. Thus, the ratio ofcis/trans cyclohexanedicarboxylate unit may be controlled within asuitable range, preferably 20/80% to 80/20%, more preferably 30/70% to70/30%, so that desirable heat resistance and transparency can beobtained.

The 1,4:3,6-dianhydrohexitol may be isomannide, isosorbide or isoidide,preferably isosorbide.

The bio-based polycarbonate ester according to the present invention maybe obtained by a preparation method comprising the steps of:

(1) subjecting a compound of formula 2 and phenol to atransesterification or esterification reaction to obtain a compound offormula 3; and

(2) subjecting the compound of formula 3 obtained in Step (1), acompound of formula 4, and 1,4:3,6-dianhydrohexitol to a polycarbonatemelt polycondensation reaction to prepare a compound comprising arepeating unit of formula 1:

wherein, in formula 1, x satisfies 0<x<1,

in formula 2, R is methyl or hydrogen, and,

in formula 4, R₁ and R₂ are each independently an aliphatic group having1 to 18 carbon atoms or an aromatic group having 6 to 20 carbon atomswhich may have an optional substituent.

In the definitions of R₁ and R₂, examples of the aliphatic group having1 to 18 carbon atoms is C₁₋₁₈ alkyl, C₂₋₁₈ alkenyl, C₂₋₁₈ alkynyl, C₃₋₁₈cycloalkyl and the like, and examples of the aromatic group having 6 to20 carbon atoms is C₆₋₂₀ aryl and the like. The R₁ and R₂ may eachindependently contains one or more heteroatoms selected from the groupconsisting of N, S and O atoms. The R₁ and R₂ may each independentlyhave one or more substituents. The substituents of R₁ and R₂ may be eachindependently C₁₋₁₀ alkyl or C₆₋₁₀ aryl which may contain one or moreheteroatoms selected from the group consisting of N, S and O atoms.

In Step (1), the compound of formula 3, i.e.,1,4-diphenyl-cyclohexanedicarboxylate, is obtained by subjecting thecompound of formula 2 and phenol to a transesterification oresterification reaction.

Specifically, dimethyl ester of DMCD (the compound of formula 2 whereinR is methyl) or dicarboxylic acid of CHDA (the compound of formula 2wherein R is H) is converted into diphenyl ester through Step (1) above,and thereby forming 1,4-diphenyl-cyclohexanedicarboxylate which can bereacted with diol to produce phenol as a byproduct via atransesterification reaction in the subsequent Step (2).

In case of DMCD and CHDA, since these compounds can react with phenol ina molten state, it is easy to manufacture DPCD.

Various compounds including primary, secondary, tertiary dicarboxylateor dicarboxylic acid may be also used together, in addition to thecompound of formula 2, depending on the desired properties, as astarting material for forming an ester bond in the polymer chain of thepresent invention. Such compounds may be converted into diphenyl esterby the reaction with phenol, and then used for polycarbonate meltpolycondensation, together with the compound of formula 3.

In this case, when the amount of diphenyl ester compound used other thanthe compound of formula 3 is z, the amount of the compound of formula 3is 1-z. As such, z satisfies 0≦z<1.

The diphenyl ester compound other than the compound of formula 3 may beone kind or a mixture of two or more kinds.

In order to give the bio-based polycarbonate ester of the presentinvention high heat resistance and transparency, and improvedweatherability and UV stability, the diphenyl ester compound other thanthe compound of formula 2 may be dicarboxylate or dicarboxylic acidhaving a single or fused saturated homocycle or heterocycle in itsmolecular center, for example, at least one dicarboxylate ordicarboxylic acid compound selected from the group consisting of:dicarboxylate such as tetrahydro-2,5-dimethyl-furandicarboxylate,1,2-dimethyl-cyclohexanedicarboxylate,1,3-dimethyl-cyclohexanedicarboxylate,decahydro-2,4-dimethyl-naphthalenedicarboxylate,decahydro-2,5-dimethyl-naphthalenedicarboxylate,decahydro-2,6-dimethyl-naphthalenedicarboxylate,decahydro-2,7-dimethyl-naphthalenedicarboxylate, and the like; anddicarboxylic acid such as tetrahydro-2,5-furandicarboxylic acid,1,2-cyclohexanedicarboxylic acid, 1,3-cyclohexanedicarboxylic acid,decahydro-2,4-naphthalenedicarboxylic acid,decahydro-2,5-naphthalenedicarboxylic acid,decahydro-2,6-naphthalenedicarboxylic acid,decahydro-2,7-naphthalenedicarboxylic acid, and the like. Such compoundsare preferably decahydro-2,6-dimethyl-naphthalenedicarboxylate ordecahydro-2,6-naphthalenedicarboxylic acid and, a compound obtainablefrom a bio-based material, tetrahydro-2,5-dimethyl-furandicarboxylate ortetrahydro-2,5-furandicarboxylic acid.

The phenyl ester substitution reaction may be conducted at 150 to 250°C. under a normal pressure, or at 150 to 300° C. under an elevatedpressure of 0.1 to 10 bar, preferably 0.5 to 5 bar. The reaction timemay be 5 minutes to 48 hours, preferably 10 minutes to 24 hours.

Phenol may be used in an amount of 2 to 50 times, preferably 4 to 20times of the total mole number of the compound of formula 2, i.e., 2 to50 times, preferably 4 to 20 times of the stoichiometric amount ofphenol required for esterification of all methyl ester (when R ismethyl) or carboxylic acid (when R is H) of the compound of formula 2.If the amount of phenol used is not within said range, the final yieldof the compound of formula 3 may be reduced.

In Step (2), the compound of formula 3 obtained in Step (1), thecompound of formula 4, and 1,4:3,6-dianhydrohexitol are subjected to apolycarbonate melt polycondensation to obtain the compound comprisingthe repeating unit of formula 1.

In Step (2), the reaction of 1,4:3,6-dianhydrohexitol with the compoundof formula 4 forms a carbonate bond (Repeating Unit 1) and the reactionof 1,4:3,6-dianhydrohexitol with the compound of formula 3 forms anester bond (Repeating Unit 2). A repeating unit containing these bondsis represented by formula 1 above.

If the amount of 1,4:3,6-dianhydrohexitol is 1 and the amount of thecompound of formula 3 is x, the amount of compound of formula 4 used canbe determined as 1-x, as shown in Reaction Scheme 2 below:

For example, in a case where a melt polycondensation is carried out byusing isosorbide (1,4:3,6-dianhydrohexitol) and diphenyl carbonate (thecompound of formula 4) so that the amount of compound of formula 3 is 0,isosorbide homopolycarbonate (Tg 160° C.) is produced. When the amountof the compound of formula 3 increases, the amount of ester bond in thepolymer chain increases as well. If the amount of the compound offormula 3 becomes 1, a melt polycondensation only takes place betweenisosorbide and the compound of formula 3, thereby producinghomopolyester (Tg 130° C.; Macromolecules, 2013, 46, 2930). FIG. 1illustrates the change in Tg of the polymers depending on the amount ofDPC.

In conclusion, the ratio of carbonate and ester bonds in the polymerchain varies depending on the added amount of the compound of formula 3.If carbonate and ester bonds coexist in the polymer chain, thepolycarbonate ester of the present invention has a higher heatresistance as compared to the copolymer polycarbonate formed betweenisosorbide and 1,4-cyclohexanedimethanol as disclosed in US 2011/0003101A1, although comprising the same amount of isosorbide. Polycarbonategenerally shows high heat resistance and good mechanical properties whencompared with polyester, but has relatively poor chemical resistance,residual stress, and molding cycle time. The polycarbonate estercomprising both carbonate and ester bonds in a single chain, however,redresses the drawbacks of each bond type and also provides someadvantages.

The 1,4:3,6-dianhydrohexitol may be isomannide, isosorbide or isoidide,preferably isosorbide.

Meanwhile, it is very important to maintain a high purity of1,4:3,6-dianhydrohexitol which is used in the melt polycondensation, inorder to obtain a high degree of polymerization for high heat resistanceand transparency, as well as excellent mechanical properties of thebio-based polycarbonate ester.

The 1,4:3,6-dianhydrohexitol may be used in the form of powder, flake orin an aqueous solution. However, an excessive exposure to air may causeoxidation and discoloration, and it may lead to dissatisfying color andmolecular weight of the final polymer. Thus, the time of exposure to airmust be minimized, and the compound must be stored with a deoxidizingagent such as an oxygen absorber after the exposure. Particularly, it isvery important to remove impurities obtained in multi-step preparationprocess of 1,4:3,6-dianhydrohexitol. During the purification of1,4:3,6-dianhydrohexitol by distillation, it is necessary to remove aliquid component containing a trace-level of acid which can be removedby an initial separation, and an alkali metal component which be removedby a residue separation. Each of these two impurities should be kept at10 ppm or lower, preferably 5 ppm or lower, more preferably 3 ppm orlower. Examples of the compound of formula 4 may be at least onecompound selected from a group consisting of dimethyl carbonate, diethylcarbonate, di-t-butyl carbonate, diphenyl carbonate, and a substituteddiphenyl carbonate (e.g., ditolyl carbonate). Since the polycarbonatemelt polycondensation reaction is carried out under a reduced pressurecondition, diphenyl carbonate and a substituted diphenyl carbonate arepreferred.

In Step (2) above, besides 1,4:3,6-dianhydrohexitol, any kind of a diolcompound may also be used, without limitation. Various compoundsincluding primary, secondary, or tertiary diol compounds may be used incombination with 1,4:3,6-dianhydrohexitol. In this case, when the amountof diol compound used other than 1,4:3,6-dianhydrohexitol is referred toas y, the added amount of 1,4:3,6-dianhydrohexitol is 1-y.

Particularly, in a case where a petrochemical-based diol compound isused, the final bio-based content (ASTM-D6866) contained in the polymerwhich is derived from 1,4:3,6-dianhydrohexitol may be at least 1%,wherein y satisfies 0≦y<0.99. In other words, the additional diolcompound may be used in an amount of less than 99 mol %, based on 100mol % of 1,4:3,6-dianhydrohexitol.

In this step, it is preferred to use a diol compound having a single orfused saturated homocycle or heterocycle in its molecular center inorder to give the polycarbonate ester high heat resistance andtransparency, and improved weatherability and UV stability. In general,heat resistance increases when the size of a ring is big and thehydroxyl groups are in a symmetrical structure. However, opticalproperties are not dependent on the ring size and the position of thehydroxyl groups, but rather vary in accordance with the properties ofeach material. When the size of the ring becomes big, it becomesdifficult to use the compound for commercial production and utilization.The diol may be selected from the group consisting of1,2-cyclohexanedimethanol, 1,3-cyclohexanedimethanol,1,4-cyclohexanedimethanol, tricyclodecandimethanol,3,9-bis(1,1-dimethyl-2-hydroxyethyl)-2,4,8,10-tetraoxaspiro[5.5]undecane,2,2-bis(4-hydroxycyclohexyl)propane, and tetrahydro-2,5-furandimethanolthat is obtainable from a bio-based material. The preferable diols are1,4-cyclohexanedimethanol, 2,2-bis(4-hydroxycyclohexyl)propane, andtetrahydro-2,5-furandimethanol.

The cis/trans ratio of the compound of formula 3 may be 1/99% to 99/1%,preferably 10/90% to 90/10%, more preferably 20/80% to 80/20%.Additionally, the cis/trans ratio of cyclohexanedicarboxylate in therepeating unit of formula 1 may be 1/99% to 99/1%, preferably 20/80% to80/20%, more preferably 30/70% to 70/30%.

When the content of trans cyclohexanedicarboxylate unit increases, heatresistance improves owing to an increase in Tg while transparencyrelatively decreases. In contrast, if the trans content decreases,transparency improves while heat resistance reduces due to a decrease inTg. Thus, the ratio of cis/trans cyclohexanedicarboxylate unit ispreferably controlled within 20/80% to 80/20%, more preferably 30/70% to70/30%, so that desirable heat resistance and transparency can beobtained.

In the melt polycondensation of Step (2), when the amount of1,4:3,6-dianhydrohexitol used is 1, the total amount of the compounds offormula 3 and formula 4 may be 0.7 to 1.3 times, preferably 0.9 to 1.1times, more preferably 0.95 to 1.05 times of the amount of1,4:3,6-dianhydrohexitol. The temperature of the melt polycondensationreaction may be elevated at a rate of 0.1 to 10° C./min, preferably 0.2to 5° C./min, more preferably 0.5 to 2° C./min. The reaction temperaturemay be 120 to 320° C., preferably 150 to 290° C., more preferably 180 to270° C., and the reaction time may be 1 to 10 hours, preferably 3 to 8hours.

Meanwhile, phenol produced as a byproduct during the meltpolycondensation should be distilled out of the reactor in order toshift the reaction equilibrium towards polycarbonate ester. Inparticular, if the rate of temperature elevation goes out of said range,the phenol may evaporate or sublime together with the raw materials. Thebio-based polycarbonate ester may be prepared via a batch or continuousprocess.

The method for manufacturing a bio-based polycarbonate ester accordingto the present invention may additionally use a catalyst for increasingthe reactivity of the melt polycondensation reaction. Any conventionalalkali metal and/or alkali earth metal catalyst commonly used for thepolycarbonate melt polycondensation may be used as such catalyst. Thecatalyst may be used in combination with a basic ammonium or amine, abasic phosphorous, or a basic boron compound. However, it is preferableto use the catalyst alone. Examples of the alkali metal catalysts mayinclude LiOH, NaOH, KOH, CsOH, Li₂CO₃, Na₂CO₃, K₂CO₃, Cs₂CO₃, LiOAc,NaOAc, KOAc, CsOAc, and the like, and examples of the alkali earth metalcatalysts may include Ca(OH)₂, Ba(OH)₂, Mg(OH)₂, Sr(OH)₂, CaCO₃, BaCO₃,MgCO₃, SrCO₃, Ca(OAc)₂, Ba(OAc)₂, Mg(OAc)₂, Sr(OAc)₂, and the like.These alkali metal and/or alkali earth metal catalysts may be used aloneor in combination of two or more.

The catalyst may be used in an amount of 0.1 to 30 μmol, preferably 0.5to 25 μmol, more preferably 0.5 to 20 μmol, per mole of the total amountof the diol (1,4:3,6-dianhydrohexitol and an additional diol) used inthe melt polycondensation reaction. Although the catalyst may beemployed at any time regardless of the progress of the meltpolycondensation reaction, it is preferable to introduce the catalystbefore the initiation of the melt polycondensation reaction. When theamount of the catalyst used is less than 0.1 μmol per mole of the totalamount of the diol, it is difficult to obtain a targeted degree ofpolymerization. If the amount of the catalyst exceeds 30 μmol, it causesside reactions and thus directly affects deterioration of targetproperties such as reduced transparency.

In addition, in the method for manufacturing a bio-based polycarbonateester according to the present invention, as the melt polycondensationreaction takes place in a molten state which has a high viscosity due tothe increase in polymerization level, it is necessary to quickly removebyproducts from the molten state. Also, temperature elevation andpressure reduction take place stepwise in order to promote the rate ofthe polymerization reaction.

After the raw materials are introduced, the first part of the reactionmay be carried out at a temperature of 130 to 250° C., preferably 140 to240° C., more preferably 150 to 230° C., for 0.1 to 10 hours, preferably0.5 to 3 hours. When the pressure is reduced in said temperature range,the reduced pressure condition may be 5 to 700 Ton, preferably 10 to 600Ton.

The second part of the reaction may be carried out at a temperature of210 to 290° C., preferably 220 to 280° C., more preferably 230 to 270°C., for 0.1 to 10 hours, preferably 0.5 to 3 hours. When the pressure isreduced in said temperature range, the reduced pressure condition may be20 Ton or less, preferably 10 Ton or less.

Additionally, the method for manufacturing a bio-based polycarbonateester according to the present invention may further comprise variousadditives, if necessary. For example, the employable additive mayinclude an antioxidant and a thermal stabilizer such as hindered phenol,hydroquinone, phosphite, and a substituted compound thereof; aUV-absorber such as resorcinol, salicylate, etc.; a color-protectingagent such as phosphite, hydrophosphite, etc.; and a lubricant such asmontanic acid, stearyl alcohol, etc. Also, a dye and pigment may be usedas a colorant; carbon black may be used as a conductive agent, colorantor nucleation agent; and a flame retardant, a plasticizer, an antistaticagent and the like may also be used. As such, the aforementionedadditives may be included in an amount that does not cause adverseeffects on the final properties of the polymer, especially ontransparency.

The bio-based polycarbonate ester comprising a repeating unit of formula1 prepared by the method for manufacturing a polycarbonate esteraccording to the present invention may have a final intrinsic viscosity(hereinafter referred to as IV) of 0.3 to 2.0 dL/g.

Hereinafter, the present invention is described more specifically byfollowing examples. However, these examples are provided only forillustration purposes, and the present invention is not limited thereto.

PREPARATION EXAMPLE 1 Synthesis of DPCD by Using CHDA

100 g (0.58 mol) of CHDA (SK Chemicals) with a cis/trans ratio of 95/5%,218 g (2.32 mol) of phenol, 0.1 g (0.55 mmol) of Zn(OAc)₂ catalyst, anda magnetic stirrer were introduced into a 500 mL one-neck flask. Adistillation head, a thermometer, and a cooling condenser were equippedto the flask, and the flask was heated to 200° C. A reaction was carriedout at the same temperature for 24 hours, and water which was generatedas a byproduct of the reaction was disposed from the flask. Uponcompletion of the reaction, the reactant thus obtained was cooled downto room temperature, and excessively introduced phenol was removedtherefrom by using an evaporator. The solid compound thus obtained wasadded with excessive water, and mechanically stirred to remove theresidual phenol. After 24 hours vacuum drying at 90° C., 111 g of DPCDwas obtained (yield: 59%). The cis/trans ratio had been changed to55/45% as a result of the reaction with phenol under the said reactionconditions: the cis content was decreased, whereas the trans content wasincreased.

PREPARATION EXAMPLE 2 Synthesis of DPCD by Using DMCD

100 g (0.50 mol) of DMCD (SK Chemicals) with a cis/trans ratio of77/23%, 188 g (2.00 mol) of phenol, 100 mL of water, and 1.0 g (5.81mmol) of p-toluensulfonic acid catalyst were introduced into a 500 mLone-neck flask, together with a magnetic stirrer. The flask was equippedwith a cooling condenser, heated to 100° C., and refluxed under stirringfor 10 hours. Upon completion of the reaction, the reactant thusobtained was cooled down to room temperature, and then water and phenolwere removed therefrom by distillation. Subsequently, the remainingreactant was heated to 200° C., and the reaction was carried out at thesame temperature for 24 hours, followed by disposing water which wasgenerated as a byproduct of the reaction. Upon completion of thereaction, the reactant thus obtained was cooled down to roomtemperature, and excessively introduced phenol was removed therefrom byusing an evaporator. The solid compound thus obtained was added withexcessive water, and mechanically stirred to remove the residual phenol.After 24 hours vacuum drying at 90° C., 86 g of DPCD was obtained(yield: 53%). The cis/trans ratio had been changed to 52/48% as a resultof the reaction with phenol under the said reaction conditions: the ciscontent was decreased, whereas the trans content was increased.

EXAMPLE 1 Preparation of Bio-Based Polycarbonate Ester

A distillation head, a thermometer, a cooling condenser, and amechanical stirrer were equipped to a 500 mL three-neck flask. 102.3 g(0.7 mol) of isosorbide (Roquette Freres), 97.3 g (0.3 mol) of DPCDobtained from Preparation Example 1, 85.7 g (0.4 mol) of DPC (Aldrich),and 5.9×10⁻⁴ g (1.8×10^(×3) mmol) of cesium carbonate (Cs₂CO₃), as acatalyst, were added to the flask and the flask was heated to 150° C.Once the temperature reached 150° C., the pressure was reduced to 400Ton, and the temperature was elevated to 190° C. over 1 hour. During thetemperature elevation, phenol started to form as a byproduct ofpolymerization reaction. When the temperature reached 190° C., thepressure was reduced to 100 Ton, maintained for 20 minutes, and then thetemperature was elevated to 230° C. over 20 minutes. Once thetemperature reached 230° C., the pressure was reduced to 10 Ton, andthen the temperature was elevated to 250° C. over 10 minutes. Thepressure was reduced to 1 Ton or less at 250° C., and the reaction wascontinued until it reached a desired stirring torque. When the stirringtorque reached the desired value, the reaction was terminated, and thetemperature was cooled down to room temperature. The cis/trans ratio ofthe cyclohexanedicarboxylate unit in the polymer chain obtained as afinal product had been changed to 40/60%. The cis content was decreased,whereas the trans content was increased, as compared to its startingmaterial DPCD. The bio-based polycarbonate ester thus prepared had Tg of143° C., and IV of 0.48 dL/g. The ¹H NMR and IR spectrum of the finalproduct are shown in FIGS. 2 and 3.

COMPARATIVE EXAMPLE 1 Preparation of Bio-Based Polycarbonate Ester byUsing CHDM

A bio-based polycarbonate ester was prepared by using the same procedureas Example 1, except for using 10.1 g (0.07 mol) of CHDM (SK Chemicals)along with DPCD and DPC, and 92.1 g (0.63 mol) of isosorbide (RoquetteFreres). The cis/trans ratio of the cyclohexanedicarboxylate unit in thepolymer chain thus obtained as a final product had been changed to38/62%. The bio-based polycarbonate ester thus prepared had Tg of 129°C., and IV of 0.51 dL/g.

COMPARATIVE EXAMPLE 2 Preparation of Isosorbide Homopolycarbonate

An isosorbide homopolycarbonate was prepared by using the same procedureas Example 1, except for using 150.0 g (0.7 mol) of DPC (Aldrich), withno use of DPCD. The isosorbide homopolycarbonate thus obtained had Tg of160° C., and IV of 0.49 dL/g.

COMPARATIVE EXAMPLE 3 Preparation of Isosorbide/DPCD Homopolyester

A bio-based isosorbide/DPCD polyester was prepared by using the sameprocedure as Example 1, except for using 227.1 (0.7 mol) of DPCD with nouse of DPC. The cis/trans ratio of the cyclohexanedicarboxylate unit inthe polymer chain thus obtained as a final product had been changed to36/64%. The bio-based polycarbonate ester thus prepared had Tg of 130°C., and IV of 0.46 dL/g.

COMPARATIVE EXAMPLE 4 Preparation of DDDA Copolymerized IsosorbidePolycarbonate Ester

A DDDA copolymerized isosorbide polycarbonate ester was prepared byusing the same procedure as Example 1, except for using 32.2 g (0.14mol) of dodecanedioic acid (hereinafter referred to as DDDA, Aldrich)instead of DPCD, and 120.0 g (0.56 mol) of DPC (Aldrich). The DDDAcopolymerized isosorbide polycarbonate ester had Tg of 121° C., and IVof 0.34 dL/g.

COMPARATIVE EXAMPLE 5 Preparation of Bio-Based Polycarbonate Ester WithHigh cis Content

A bio-based polycarbonate ester was prepared by using the same procedureas Example 1, except for using 97.3 g (0.3 mol) of DPCD having acis/trans ratio of 90/10%. The cis/trans ratio of thecyclohexanedicarboxylate unit in the polymer chain thus obtained as afinal product had been changed to 85/15%. The bio-based polycarbonateester thus prepared had Tg of 113° C., and IV of 0.37 dL/g.

<Light Transmittance Measurement>

The light transmittance of sheets prepared from the copolymerizedsamples obtained in Example 1 and Comparative Examples 1 to 5 in thevisible range was measured by using a UV-VIS spectrometer in the rangeof 200 to 800 nm.

The content ratios and the property test results of the polymer samplesobtained in Example 1 and Comparative Examples 1 to 5 are shown in Table1 below.

TABLE 1 ISB CHDM cis/ c¹- e²- c¹- e²- e²- e²- trans Tg T³ ISB CHDM DPCDDDDA DPC ISB ISB CHDM CHDM CD DD (%) (° C.) (%) Ex. 1 1 0 0.6 0 0.4 0.40.3 0 0 0.3 0 40/60 143 92 Comp. 0.9 0.1 0.6 0 0.4 0.36 0.27 0.04 0.030.3 0 38/62 129 91 Ex. 1 Comp. 1 0 0 0 1 1 0 0 0 0 0 — 160 89 Ex. 2Comp. 1 0 1 0 0 0 0.5 0 0 0.5 0 36/64 130 89 Ex. 3 Comp. 1 0 0 0.2 0.80.8 0.1 0 0 0 0.1 — 121 87 Ex. 4 Comp. 1 0 0.6 0 0.4 0.4 0.3 0 0 0.3 085/15 113 90 Ex. 5 ¹c, carbonate; ²e, ester; ³T, transmittance; CD:cyclohexanedicarboxylate; DD: dodecanedioate.

As shown in Table 1 above, when a bio-based polycarbonate ester wasprepared from 1,4-diphenyl-cyclohexanedicarboxylate of formula 3 whichwas prepared according to the inventive method, the bio-basedpolycarbonate ester exhibits improved heat resistance as compared to aconventional biopolycarbonate prepared from 1,4:3,6-dianhydrohexitol and1,4-cyclohexanedimethanol, although comprising the same amount ofisosorbide. The inventive polycarbonate ester has an advantage that theamount of isosorbide in the polymer can be reduced owing to improvedheat resistance.

Also, in case of Comparative Example 4, the optical transmittance levelwas dropped down from highly transparent poly(methyl methacrylate)(PMMA) level to a general BPA-based polycarbonate level due to thepresence of a long chain aliphatic diacid which induces an increase inthe photoelastic coefficient, and it was also found that the glasstransition temperature was relatively low.

In particular, in case of Comparative Example 5, the glass transitiontemperature was significantly decreased as compared to Example 1 due tothe high cis content of cyclohexanedicarboxylate unit in the polymerchain so obtained, and it was also confirmed that the opticaltransmittance level was reduced.

Accordingly, it is possible to control the properties deriving from thecarbonate bond and the ester bond by adjusting the ratio thereof to givea desirable property according to its needs. Therefore, thepolycarbonate ester prepared according to the present invention exhibitshigh heat resistance and transparency, and thus can be useful in variousapplications, e.g., glass alternative for automobile, optical lens andfilm, feeding bottle, food container, etc.

1-5. (canceled)
 6. A method for manufacturing a bio-based polycarbonateester comprising: (1) subjecting a compound of Formula 2 and phenol to atransesterification or esterification reaction to obtain a compound ofFormula 3; and (2) subjecting the compound of Formula 3 obtained in Step(1), a compound of Formula 4, and 1,4:3,6-dianhydrohexitol to apolycarbonate melt polycondensation reaction to prepare a compoundcomprising a repeating unit of Formula 1:

wherein, in Formula 1, x satisfies 0<x<1, in Formula 2, R is methyl orhydrogen, and in Formula 4, R₁ and R₂ are each independently analiphatic group having 1 to 18 carbon atoms or an aromatic group having6 to 20 carbon atoms which may have an optional substituent.
 7. Themethod of claim 6, wherein the ratio of cis/transcyclohexanedicarboxylate unit is 1/99% to 99/1% in the repeating unit ofFormula
 1. 8. The method of claim 6, wherein the transesterification oresterification of Step (1) takes place in the presence of at least onedicarboxylate or dicarboxylic acid compound selected from the groupconsisting of tetrahydro-2,5-dimethyl-furandicarboxylate,1,2-dimethyl-cyclohexanedicarboxylate,1,3-dimethyl-cyclohexanedicarboxylate,decahydro-2,4-dimethyl-naphthalenedicarboxylate,decahydro-2,5-dimethyl-naphthalenedicarboxylate,decahydro-2,6-dimethyl-naphthalenedicarboxylate,decahydro-2,7-dimethyl-naphthalenedicarboxylate,tetrahydro-2,5-furandicarboxylic acid, 1,2-cyclohexanedicarboxylic acid,1,3-cyclohexanedicarboxylic acid, decahydro-2,4-naphthalenedicarboxylicacid, decahydro-2,5-naphthalenedicarboxylic acid,decahydro-2,6-naphthalenedicarboxylic acid, anddecahydro-2,7-naphthalenedicarboxylic acid.
 9. The method of claim 6,wherein the melt polycondensation of Step (2) takes place in thepresence of a diol compound selected from the group consisting of1,2-cyclohexanedimethanol, 1,3-cyclohexanedimethanol,1,4-cyclohexanedimethanol, tricyclodecandimethanol,3,9-bis(1,1-dimethyl-2-hydroxyethyl)-2,4,8,10-tetraoxaspiro[5.5]undecane,2,2-bis(4-hydroxycyclohexyl)propane, and tetrahydro-2,5-furandimethanolthat is obtainable from a bio-based material.
 10. The method of claim 9,wherein the diol compound is used in an amount of less than 99 mol %,based on 100 mol % of 1,4:3,6-dianhydrohexitol.
 11. The method of claim6, wherein the reaction in Step (1) is conducted at 150 to 250° C. undera normal pressure, or at 150 to 300° C. under an elevated pressure of0.1 to 10 bar, for 5 minutes to 48 hours.
 12. The method of claim 6,wherein phenol is used in Step (1) in an amount of 2 to 50 times of thetotal mole number of the compound of Formula
 2. 13. The method of claim6, wherein the compound of Formula 4 is dimethyl carbonate, diethylcarbonate, di-t-butyl carbonate, diphenyl carbonate, or ditolylcarbonate.
 14. The method of claim 6, wherein the melt polycondensationof Step (2) includes a first part of the reaction and a second part ofthe reaction, the first part of the reaction is carried out under areduced pressure of 5 to 700 Torr at a temperature of 130 to 250° C. for0.1 to 10 hours, and the second part of the reaction is carried outunder a reduced pressure of 20 Torr or less at a temperature of 210 to290° C. for 0.1 to 10 hours.
 15. The method of claim 6, wherein thecompound of Formula 3 is obtained by a reaction of1,4-dimethyl-cyclohexane dicarboxylate or 1,4-cyclohexanedicarboxylicacid with phenol.